JPS60262990A - Wet electrolytic refining method of metallic titanium - Google Patents
Wet electrolytic refining method of metallic titaniumInfo
- Publication number
- JPS60262990A JPS60262990A JP59116585A JP11658584A JPS60262990A JP S60262990 A JPS60262990 A JP S60262990A JP 59116585 A JP59116585 A JP 59116585A JP 11658584 A JP11658584 A JP 11658584A JP S60262990 A JPS60262990 A JP S60262990A
- Authority
- JP
- Japan
- Prior art keywords
- soln
- tio2
- tio
- strong acid
- filtrate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
Description
【発明の詳細な説明】
本発明は、鉱石還元方法に於て化学反応の誘起まで僅か
の外部加熱のみに止り、反応誘起後は発熱化学反応の自
然発生熱のみにより、還元反応を進行させ得ることに特
徴を有するものであり、著しい熱経済と省エネルギーに
貢献するものである。[Detailed description of the invention] In the ore reduction method of the present invention, only a slight external heating is required until the chemical reaction is induced, and after the reaction is induced, the reduction reaction can proceed only by the naturally generated heat of the exothermic chemical reaction. It has particular characteristics and contributes to remarkable thermal economy and energy saving.
先づ原鉱石を微粉砕し、同様微粉砕のアルミニウム粉を
各150メノシ以上の微粉状で良く混和し、これを耐熱
性容器に収め、容器の外部下端面より加熱するが、内容
混合体に化学反応が誘起されれば、この加熱は直ちに中
止する。誘起された化学反応は著しい高発熱反応で、発
生熱による自然加熱で容器の底部から誘起された発熱反
応は、其の発生熱による還元化学反応が容器の底部に先
づ横断面的層状に発生し、この還元反応が、時間の経過
と共に逐次層状に上方へ進行して、遂に混合体の最上部
、空気に接する部分に至って全還元反応は完了する。こ
の反応では、鉱石に含有された二酸化チタンの大部分は
、アルミニウムによって還元され、−酸化チタンに変化
するが、金属の状態までは還元されない。First, the raw ore is finely ground, and the similarly finely ground aluminum powder is mixed well in the form of a fine powder of 150 or more grains each. This is placed in a heat-resistant container and heated from the external lower end of the container, but the contents of the mixture do not change. If a chemical reaction is induced, this heating is immediately stopped. The induced chemical reaction is a remarkable high-exothermic reaction, and the exothermic reaction induced from the bottom of the container due to natural heating due to the generated heat is caused by the reduction chemical reaction occurring first in a cross-sectional layer at the bottom of the container. However, as time passes, this reduction reaction progresses upward in layers, and finally reaches the top of the mixture, the part in contact with air, where the entire reduction reaction is completed. In this reaction, most of the titanium dioxide contained in the ore is reduced by aluminum and changed to -titanium oxide, but is not reduced to a metal state.
3Ti02 + 27v=k1203 +3Ti0生成
−酸化チタンは強酸に可溶であるから、耐酸容器中の強
酸液中へ化学反応終了後の混合体を投入、攪拌して溶解
し、溶解完了後濾過する。この抽出濾過液中には、少量
の鉄分等の不純物を含むため、これが除去の目的で先づ
強還元性薬剤、例えばチオグリコール酸の如き薬剤の少
量を添加して後、アルカリ性溶液を少しづつ徐々に加え
て中和する。この際、強還元性薬剤の存在のため、鉄の
水酸化物の沈澱生成反応は中性溶液完了の中和までに完
結する。従ってこの液を中和完了の時点に於て濾過すれ
ば、比較的に純度良好のチタン化合物溶液が得られる。3Ti02 + 27v=k1203 +3Ti0 production - Since titanium oxide is soluble in strong acid, the mixture after the chemical reaction is poured into a strong acid solution in an acid-resistant container, stirred and dissolved, and after the dissolution is completed, it is filtered. This extracted filtrate contains a small amount of impurities such as iron, so in order to remove these impurities, a small amount of a strong reducing agent, such as thioglycolic acid, is first added, and then an alkaline solution is added little by little. Add gradually to neutralize. At this time, due to the presence of a strong reducing agent, the precipitation-forming reaction of iron hydroxide is completed by the time the neutralization of the neutral solution is completed. Therefore, if this liquid is filtered upon completion of neutralization, a titanium compound solution with relatively good purity can be obtained.
かくの如くして得た濾液へ、更に過剰のアルカリ液を加
えて強アルカリ液とするか、或は強酸を加えて強酸性液
とするか、何れかの液を電解液とし不溶解性陽極により
通電電解して、陰極に純金属チタンを析出させる、金属
チタンの湿式電解製錬法。To the filtrate thus obtained, either an excess of alkaline solution is added to make a strong alkaline solution, or a strong acid is added to make a strong acidic solution, or either solution is used as an electrolyte and used as an insoluble anode. A wet electrolytic smelting method for titanium metal, in which pure titanium metal is deposited on the cathode through electrical electrolysis.
−屯舛=−Tunmasu=
Claims (1)
混和し、耐熱性容器に収め、その下端部を加熱し、内容
混合粉状体をして発熱化学反応を起させ、反応終了後、
耐強酸性容器に収容しである強酸性液中へ投入、溶解終
了を待って濾過、この濾液へ強還元力の薬剤を加えて後
アルカリ性液を加えて中性とし、生じた沈澱を濾過、中
性濾過液を得。この濾液を強酸により酸性液とする方法
か、或は更に過剰のアルカリにより、アルカリ性液とす
る方法か、何れかの方法の溶液を不溶解性陽極により電
解、陰極に純金属チタンを析出させる、金属チタンの湿
式%式%Finely grind raw ore, add fine aluminum powder, mix well, place in a heat-resistant container, heat the bottom end, mix the contents into powder, and cause an exothermic chemical reaction. After the reaction is complete,
Pour into a strong acidic solution stored in a strong acid-resistant container, wait until dissolution is complete, and filter. Add a strong reducing agent to this filtrate, then add an alkaline solution to make it neutral, and filter the resulting precipitate. Obtain a neutral filtrate. This filtrate is made into an acidic solution with a strong acid, or an alkaline solution is made with an excess of alkali, the solution is electrolyzed with an insoluble anode, and pure metal titanium is deposited on the cathode. Wet % formula % of metal titanium
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59116585A JPS60262990A (en) | 1984-06-08 | 1984-06-08 | Wet electrolytic refining method of metallic titanium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59116585A JPS60262990A (en) | 1984-06-08 | 1984-06-08 | Wet electrolytic refining method of metallic titanium |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60262990A true JPS60262990A (en) | 1985-12-26 |
Family
ID=14690773
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59116585A Pending JPS60262990A (en) | 1984-06-08 | 1984-06-08 | Wet electrolytic refining method of metallic titanium |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60262990A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2018048402A (en) * | 2011-12-22 | 2018-03-29 | ユニヴァーサル テクニカル リソース サービシーズ インコーポレイテッド | Apparatus and method for extraction and refining of titanium |
-
1984
- 1984-06-08 JP JP59116585A patent/JPS60262990A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2018048402A (en) * | 2011-12-22 | 2018-03-29 | ユニヴァーサル テクニカル リソース サービシーズ インコーポレイテッド | Apparatus and method for extraction and refining of titanium |
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